Mass Transfer in Irrigated Plane-Parallel Channels at Uniflow Laminar Motion of Liquid and Gas

Abstract Hydrodynamics and mass transfer in regular film apparatuses containing flat irrigated channels with a laminar flow of gas and liquid as the principal element are studied. The problem is solved by the approximate method, which makes it possible to drastically decrease the amount of the requi...
Ausführliche Beschreibung

Gespeichert in:

Autor*in:	Babak, V. N. [verfasserIn]

Format:	E-Artikel
Sprache:	Englisch

Erschienen:	2019

Übergeordnetes Werk:	Enthalten in: Theoretical foundations of chemical engineering - Moscow : MAIK Nauka/Interperiodica Publ., 2000, 53(2019), 6 vom: Nov., Seite 984-995
Übergeordnetes Werk:	volume:53 ; year:2019 ; number:6 ; month:11 ; pages:984-995

Links:	Volltext

DOI / URN:	10.1134/S0040579519050269

Katalog-ID:	SPR017987660

Internformat


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520			\|a Abstract Hydrodynamics and mass transfer in regular film apparatuses containing flat irrigated channels with a laminar flow of gas and liquid as the principal element are studied. The problem is solved by the approximate method, which makes it possible to drastically decrease the amount of the required calculations. It is proven that it is sufficient to determine the dimensionless flux as the function of dimensionless length in a restricted domain of parameters. Approximations are permissible outside the bounds of this domain: in some cases the changes of concentrations in phases along the crosswise direction can be neglected and, in other instances, the concentration changes can be neglected in the whole active mass-transfer region; i.e., diffusion layers exist in one or another phase before the estimation of concentration equilibrium in the system. Finally, the mass transfer resistance is concentrated in liquid or gas; there are parameter spaces where the change of concentration in one of the phases in a crosswise direction can be neglected, while another one contains diffusion boundary layers.
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912			\|a GBV_ILN_23
912			\|a GBV_ILN_24
912			\|a GBV_ILN_31
912			\|a GBV_ILN_32
912			\|a GBV_ILN_39
912			\|a GBV_ILN_40
912			\|a GBV_ILN_60
912			\|a GBV_ILN_62
912			\|a GBV_ILN_63
912			\|a GBV_ILN_69
912			\|a GBV_ILN_70
912			\|a GBV_ILN_73
912			\|a GBV_ILN_74
912			\|a GBV_ILN_90
912			\|a GBV_ILN_95
912			\|a GBV_ILN_100
912			\|a GBV_ILN_105
912			\|a GBV_ILN_110
912			\|a GBV_ILN_120
912			\|a GBV_ILN_138
912			\|a GBV_ILN_150
912			\|a GBV_ILN_151
912			\|a GBV_ILN_152
912			\|a GBV_ILN_161
912			\|a GBV_ILN_170
912			\|a GBV_ILN_171
912			\|a GBV_ILN_187
912			\|a GBV_ILN_206
912			\|a GBV_ILN_213
912			\|a GBV_ILN_224
912			\|a GBV_ILN_230
912			\|a GBV_ILN_250
912			\|a GBV_ILN_281
912			\|a GBV_ILN_285
912			\|a GBV_ILN_293
912			\|a GBV_ILN_370
912			\|a GBV_ILN_602
912			\|a GBV_ILN_636
912			\|a GBV_ILN_702
912			\|a GBV_ILN_2001
912			\|a GBV_ILN_2003
912			\|a GBV_ILN_2004
912			\|a GBV_ILN_2005
912			\|a GBV_ILN_2006
912			\|a GBV_ILN_2007
912			\|a GBV_ILN_2008
912			\|a GBV_ILN_2009
912			\|a GBV_ILN_2010
912			\|a GBV_ILN_2011
912			\|a GBV_ILN_2014
912			\|a GBV_ILN_2015
912			\|a GBV_ILN_2020
912			\|a GBV_ILN_2021
912			\|a GBV_ILN_2025
912			\|a GBV_ILN_2026
912			\|a GBV_ILN_2027
912			\|a GBV_ILN_2031
912			\|a GBV_ILN_2034
912			\|a GBV_ILN_2037
912			\|a GBV_ILN_2038
912			\|a GBV_ILN_2039
912			\|a GBV_ILN_2044
912			\|a GBV_ILN_2048
912			\|a GBV_ILN_2049
912			\|a GBV_ILN_2050
912			\|a GBV_ILN_2055
912			\|a GBV_ILN_2056
912			\|a GBV_ILN_2057
912			\|a GBV_ILN_2059
912			\|a GBV_ILN_2061
912			\|a GBV_ILN_2064
912			\|a GBV_ILN_2065
912			\|a GBV_ILN_2068
912			\|a GBV_ILN_2070
912			\|a GBV_ILN_2086
912			\|a GBV_ILN_2088
912			\|a GBV_ILN_2093
912			\|a GBV_ILN_2106
912			\|a GBV_ILN_2107
912			\|a GBV_ILN_2108
912			\|a GBV_ILN_2110
912			\|a GBV_ILN_2111
912			\|a GBV_ILN_2112
912			\|a GBV_ILN_2113
912			\|a GBV_ILN_2116
912			\|a GBV_ILN_2118
912			\|a GBV_ILN_2119
912			\|a GBV_ILN_2122
912			\|a GBV_ILN_2129
912			\|a GBV_ILN_2143
912			\|a GBV_ILN_2144
912			\|a GBV_ILN_2147
912			\|a GBV_ILN_2148
912			\|a GBV_ILN_2152
912			\|a GBV_ILN_2153
912			\|a GBV_ILN_2188
912			\|a GBV_ILN_2190
912			\|a GBV_ILN_2232
912			\|a GBV_ILN_2336
912			\|a GBV_ILN_2446
912			\|a GBV_ILN_2470
912			\|a GBV_ILN_2472
912			\|a GBV_ILN_2507
912			\|a GBV_ILN_2522
912			\|a GBV_ILN_2548
912			\|a GBV_ILN_4035
912			\|a GBV_ILN_4037
912			\|a GBV_ILN_4046
912			\|a GBV_ILN_4112
912			\|a GBV_ILN_4125
912			\|a GBV_ILN_4242
912			\|a GBV_ILN_4246
912			\|a GBV_ILN_4249
912			\|a GBV_ILN_4251
912			\|a GBV_ILN_4305
912			\|a GBV_ILN_4306
912			\|a GBV_ILN_4307
912			\|a GBV_ILN_4313
912			\|a GBV_ILN_4322
912			\|a GBV_ILN_4323
912			\|a GBV_ILN_4324
912			\|a GBV_ILN_4325
912			\|a GBV_ILN_4326
912			\|a GBV_ILN_4333
912			\|a GBV_ILN_4334
912			\|a GBV_ILN_4335
912			\|a GBV_ILN_4336
912			\|a GBV_ILN_4338
912			\|a GBV_ILN_4393
912			\|a GBV_ILN_4700
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952			\|d 53 \|j 2019 \|e 6 \|c 11 \|h 984-995

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allfields	10.1134/S0040579519050269 doi (DE-627)SPR017987660 (SPR)S0040579519050269-e DE-627 ger DE-627 rakwb eng 660 ASE 58.00 bkl Babak, V. N. verfasserin aut Mass Transfer in Irrigated Plane-Parallel Channels at Uniflow Laminar Motion of Liquid and Gas 2019 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier Abstract Hydrodynamics and mass transfer in regular film apparatuses containing flat irrigated channels with a laminar flow of gas and liquid as the principal element are studied. The problem is solved by the approximate method, which makes it possible to drastically decrease the amount of the required calculations. It is proven that it is sufficient to determine the dimensionless flux as the function of dimensionless length in a restricted domain of parameters. Approximations are permissible outside the bounds of this domain: in some cases the changes of concentrations in phases along the crosswise direction can be neglected and, in other instances, the concentration changes can be neglected in the whole active mass-transfer region; i.e., diffusion layers exist in one or another phase before the estimation of concentration equilibrium in the system. Finally, the mass transfer resistance is concentrated in liquid or gas; there are parameter spaces where the change of concentration in one of the phases in a crosswise direction can be neglected, while another one contains diffusion boundary layers. Enthalten in Theoretical foundations of chemical engineering Moscow : MAIK Nauka/Interperiodica Publ., 2000 53(2019), 6 vom: Nov., Seite 984-995 (DE-627)332339645 (DE-600)2053532-6 1608-3431 nnns volume:53 year:2019 number:6 month:11 pages:984-995 https://dx.doi.org/10.1134/S0040579519050269 lizenzpflichtig Volltext GBV_USEFLAG_A SYSFLAG_A GBV_SPRINGER SSG-OLC-PHA GBV_ILN_11 GBV_ILN_20 GBV_ILN_22 GBV_ILN_23 GBV_ILN_24 GBV_ILN_31 GBV_ILN_32 GBV_ILN_39 GBV_ILN_40 GBV_ILN_60 GBV_ILN_62 GBV_ILN_63 GBV_ILN_69 GBV_ILN_70 GBV_ILN_73 GBV_ILN_74 GBV_ILN_90 GBV_ILN_95 GBV_ILN_100 GBV_ILN_105 GBV_ILN_110 GBV_ILN_120 GBV_ILN_138 GBV_ILN_150 GBV_ILN_151 GBV_ILN_152 GBV_ILN_161 GBV_ILN_170 GBV_ILN_171 GBV_ILN_187 GBV_ILN_206 GBV_ILN_213 GBV_ILN_224 GBV_ILN_230 GBV_ILN_250 GBV_ILN_281 GBV_ILN_285 GBV_ILN_293 GBV_ILN_370 GBV_ILN_602 GBV_ILN_636 GBV_ILN_702 GBV_ILN_2001 GBV_ILN_2003 GBV_ILN_2004 GBV_ILN_2005 GBV_ILN_2006 GBV_ILN_2007 GBV_ILN_2008 GBV_ILN_2009 GBV_ILN_2010 GBV_ILN_2011 GBV_ILN_2014 GBV_ILN_2015 GBV_ILN_2020 GBV_ILN_2021 GBV_ILN_2025 GBV_ILN_2026 GBV_ILN_2027 GBV_ILN_2031 GBV_ILN_2034 GBV_ILN_2037 GBV_ILN_2038 GBV_ILN_2039 GBV_ILN_2044 GBV_ILN_2048 GBV_ILN_2049 GBV_ILN_2050 GBV_ILN_2055 GBV_ILN_2056 GBV_ILN_2057 GBV_ILN_2059 GBV_ILN_2061 GBV_ILN_2064 GBV_ILN_2065 GBV_ILN_2068 GBV_ILN_2070 GBV_ILN_2086 GBV_ILN_2088 GBV_ILN_2093 GBV_ILN_2106 GBV_ILN_2107 GBV_ILN_2108 GBV_ILN_2110 GBV_ILN_2111 GBV_ILN_2112 GBV_ILN_2113 GBV_ILN_2116 GBV_ILN_2118 GBV_ILN_2119 GBV_ILN_2122 GBV_ILN_2129 GBV_ILN_2143 GBV_ILN_2144 GBV_ILN_2147 GBV_ILN_2148 GBV_ILN_2152 GBV_ILN_2153 GBV_ILN_2188 GBV_ILN_2190 GBV_ILN_2232 GBV_ILN_2336 GBV_ILN_2446 GBV_ILN_2470 GBV_ILN_2472 GBV_ILN_2507 GBV_ILN_2522 GBV_ILN_2548 GBV_ILN_4035 GBV_ILN_4037 GBV_ILN_4046 GBV_ILN_4112 GBV_ILN_4125 GBV_ILN_4242 GBV_ILN_4246 GBV_ILN_4249 GBV_ILN_4251 GBV_ILN_4305 GBV_ILN_4306 GBV_ILN_4307 GBV_ILN_4313 GBV_ILN_4322 GBV_ILN_4323 GBV_ILN_4324 GBV_ILN_4325 GBV_ILN_4326 GBV_ILN_4333 GBV_ILN_4334 GBV_ILN_4335 GBV_ILN_4336 GBV_ILN_4338 GBV_ILN_4393 GBV_ILN_4700 58.00 ASE AR 53 2019 6 11 984-995
spelling	10.1134/S0040579519050269 doi (DE-627)SPR017987660 (SPR)S0040579519050269-e DE-627 ger DE-627 rakwb eng 660 ASE 58.00 bkl Babak, V. N. verfasserin aut Mass Transfer in Irrigated Plane-Parallel Channels at Uniflow Laminar Motion of Liquid and Gas 2019 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier Abstract Hydrodynamics and mass transfer in regular film apparatuses containing flat irrigated channels with a laminar flow of gas and liquid as the principal element are studied. The problem is solved by the approximate method, which makes it possible to drastically decrease the amount of the required calculations. It is proven that it is sufficient to determine the dimensionless flux as the function of dimensionless length in a restricted domain of parameters. Approximations are permissible outside the bounds of this domain: in some cases the changes of concentrations in phases along the crosswise direction can be neglected and, in other instances, the concentration changes can be neglected in the whole active mass-transfer region; i.e., diffusion layers exist in one or another phase before the estimation of concentration equilibrium in the system. Finally, the mass transfer resistance is concentrated in liquid or gas; there are parameter spaces where the change of concentration in one of the phases in a crosswise direction can be neglected, while another one contains diffusion boundary layers. Enthalten in Theoretical foundations of chemical engineering Moscow : MAIK Nauka/Interperiodica Publ., 2000 53(2019), 6 vom: Nov., Seite 984-995 (DE-627)332339645 (DE-600)2053532-6 1608-3431 nnns volume:53 year:2019 number:6 month:11 pages:984-995 https://dx.doi.org/10.1134/S0040579519050269 lizenzpflichtig Volltext GBV_USEFLAG_A SYSFLAG_A GBV_SPRINGER SSG-OLC-PHA GBV_ILN_11 GBV_ILN_20 GBV_ILN_22 GBV_ILN_23 GBV_ILN_24 GBV_ILN_31 GBV_ILN_32 GBV_ILN_39 GBV_ILN_40 GBV_ILN_60 GBV_ILN_62 GBV_ILN_63 GBV_ILN_69 GBV_ILN_70 GBV_ILN_73 GBV_ILN_74 GBV_ILN_90 GBV_ILN_95 GBV_ILN_100 GBV_ILN_105 GBV_ILN_110 GBV_ILN_120 GBV_ILN_138 GBV_ILN_150 GBV_ILN_151 GBV_ILN_152 GBV_ILN_161 GBV_ILN_170 GBV_ILN_171 GBV_ILN_187 GBV_ILN_206 GBV_ILN_213 GBV_ILN_224 GBV_ILN_230 GBV_ILN_250 GBV_ILN_281 GBV_ILN_285 GBV_ILN_293 GBV_ILN_370 GBV_ILN_602 GBV_ILN_636 GBV_ILN_702 GBV_ILN_2001 GBV_ILN_2003 GBV_ILN_2004 GBV_ILN_2005 GBV_ILN_2006 GBV_ILN_2007 GBV_ILN_2008 GBV_ILN_2009 GBV_ILN_2010 GBV_ILN_2011 GBV_ILN_2014 GBV_ILN_2015 GBV_ILN_2020 GBV_ILN_2021 GBV_ILN_2025 GBV_ILN_2026 GBV_ILN_2027 GBV_ILN_2031 GBV_ILN_2034 GBV_ILN_2037 GBV_ILN_2038 GBV_ILN_2039 GBV_ILN_2044 GBV_ILN_2048 GBV_ILN_2049 GBV_ILN_2050 GBV_ILN_2055 GBV_ILN_2056 GBV_ILN_2057 GBV_ILN_2059 GBV_ILN_2061 GBV_ILN_2064 GBV_ILN_2065 GBV_ILN_2068 GBV_ILN_2070 GBV_ILN_2086 GBV_ILN_2088 GBV_ILN_2093 GBV_ILN_2106 GBV_ILN_2107 GBV_ILN_2108 GBV_ILN_2110 GBV_ILN_2111 GBV_ILN_2112 GBV_ILN_2113 GBV_ILN_2116 GBV_ILN_2118 GBV_ILN_2119 GBV_ILN_2122 GBV_ILN_2129 GBV_ILN_2143 GBV_ILN_2144 GBV_ILN_2147 GBV_ILN_2148 GBV_ILN_2152 GBV_ILN_2153 GBV_ILN_2188 GBV_ILN_2190 GBV_ILN_2232 GBV_ILN_2336 GBV_ILN_2446 GBV_ILN_2470 GBV_ILN_2472 GBV_ILN_2507 GBV_ILN_2522 GBV_ILN_2548 GBV_ILN_4035 GBV_ILN_4037 GBV_ILN_4046 GBV_ILN_4112 GBV_ILN_4125 GBV_ILN_4242 GBV_ILN_4246 GBV_ILN_4249 GBV_ILN_4251 GBV_ILN_4305 GBV_ILN_4306 GBV_ILN_4307 GBV_ILN_4313 GBV_ILN_4322 GBV_ILN_4323 GBV_ILN_4324 GBV_ILN_4325 GBV_ILN_4326 GBV_ILN_4333 GBV_ILN_4334 GBV_ILN_4335 GBV_ILN_4336 GBV_ILN_4338 GBV_ILN_4393 GBV_ILN_4700 58.00 ASE AR 53 2019 6 11 984-995
allfields_unstemmed	10.1134/S0040579519050269 doi (DE-627)SPR017987660 (SPR)S0040579519050269-e DE-627 ger DE-627 rakwb eng 660 ASE 58.00 bkl Babak, V. N. verfasserin aut Mass Transfer in Irrigated Plane-Parallel Channels at Uniflow Laminar Motion of Liquid and Gas 2019 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier Abstract Hydrodynamics and mass transfer in regular film apparatuses containing flat irrigated channels with a laminar flow of gas and liquid as the principal element are studied. The problem is solved by the approximate method, which makes it possible to drastically decrease the amount of the required calculations. It is proven that it is sufficient to determine the dimensionless flux as the function of dimensionless length in a restricted domain of parameters. Approximations are permissible outside the bounds of this domain: in some cases the changes of concentrations in phases along the crosswise direction can be neglected and, in other instances, the concentration changes can be neglected in the whole active mass-transfer region; i.e., diffusion layers exist in one or another phase before the estimation of concentration equilibrium in the system. Finally, the mass transfer resistance is concentrated in liquid or gas; there are parameter spaces where the change of concentration in one of the phases in a crosswise direction can be neglected, while another one contains diffusion boundary layers. Enthalten in Theoretical foundations of chemical engineering Moscow : MAIK Nauka/Interperiodica Publ., 2000 53(2019), 6 vom: Nov., Seite 984-995 (DE-627)332339645 (DE-600)2053532-6 1608-3431 nnns volume:53 year:2019 number:6 month:11 pages:984-995 https://dx.doi.org/10.1134/S0040579519050269 lizenzpflichtig Volltext GBV_USEFLAG_A SYSFLAG_A GBV_SPRINGER SSG-OLC-PHA GBV_ILN_11 GBV_ILN_20 GBV_ILN_22 GBV_ILN_23 GBV_ILN_24 GBV_ILN_31 GBV_ILN_32 GBV_ILN_39 GBV_ILN_40 GBV_ILN_60 GBV_ILN_62 GBV_ILN_63 GBV_ILN_69 GBV_ILN_70 GBV_ILN_73 GBV_ILN_74 GBV_ILN_90 GBV_ILN_95 GBV_ILN_100 GBV_ILN_105 GBV_ILN_110 GBV_ILN_120 GBV_ILN_138 GBV_ILN_150 GBV_ILN_151 GBV_ILN_152 GBV_ILN_161 GBV_ILN_170 GBV_ILN_171 GBV_ILN_187 GBV_ILN_206 GBV_ILN_213 GBV_ILN_224 GBV_ILN_230 GBV_ILN_250 GBV_ILN_281 GBV_ILN_285 GBV_ILN_293 GBV_ILN_370 GBV_ILN_602 GBV_ILN_636 GBV_ILN_702 GBV_ILN_2001 GBV_ILN_2003 GBV_ILN_2004 GBV_ILN_2005 GBV_ILN_2006 GBV_ILN_2007 GBV_ILN_2008 GBV_ILN_2009 GBV_ILN_2010 GBV_ILN_2011 GBV_ILN_2014 GBV_ILN_2015 GBV_ILN_2020 GBV_ILN_2021 GBV_ILN_2025 GBV_ILN_2026 GBV_ILN_2027 GBV_ILN_2031 GBV_ILN_2034 GBV_ILN_2037 GBV_ILN_2038 GBV_ILN_2039 GBV_ILN_2044 GBV_ILN_2048 GBV_ILN_2049 GBV_ILN_2050 GBV_ILN_2055 GBV_ILN_2056 GBV_ILN_2057 GBV_ILN_2059 GBV_ILN_2061 GBV_ILN_2064 GBV_ILN_2065 GBV_ILN_2068 GBV_ILN_2070 GBV_ILN_2086 GBV_ILN_2088 GBV_ILN_2093 GBV_ILN_2106 GBV_ILN_2107 GBV_ILN_2108 GBV_ILN_2110 GBV_ILN_2111 GBV_ILN_2112 GBV_ILN_2113 GBV_ILN_2116 GBV_ILN_2118 GBV_ILN_2119 GBV_ILN_2122 GBV_ILN_2129 GBV_ILN_2143 GBV_ILN_2144 GBV_ILN_2147 GBV_ILN_2148 GBV_ILN_2152 GBV_ILN_2153 GBV_ILN_2188 GBV_ILN_2190 GBV_ILN_2232 GBV_ILN_2336 GBV_ILN_2446 GBV_ILN_2470 GBV_ILN_2472 GBV_ILN_2507 GBV_ILN_2522 GBV_ILN_2548 GBV_ILN_4035 GBV_ILN_4037 GBV_ILN_4046 GBV_ILN_4112 GBV_ILN_4125 GBV_ILN_4242 GBV_ILN_4246 GBV_ILN_4249 GBV_ILN_4251 GBV_ILN_4305 GBV_ILN_4306 GBV_ILN_4307 GBV_ILN_4313 GBV_ILN_4322 GBV_ILN_4323 GBV_ILN_4324 GBV_ILN_4325 GBV_ILN_4326 GBV_ILN_4333 GBV_ILN_4334 GBV_ILN_4335 GBV_ILN_4336 GBV_ILN_4338 GBV_ILN_4393 GBV_ILN_4700 58.00 ASE AR 53 2019 6 11 984-995
allfieldsGer	10.1134/S0040579519050269 doi (DE-627)SPR017987660 (SPR)S0040579519050269-e DE-627 ger DE-627 rakwb eng 660 ASE 58.00 bkl Babak, V. N. verfasserin aut Mass Transfer in Irrigated Plane-Parallel Channels at Uniflow Laminar Motion of Liquid and Gas 2019 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier Abstract Hydrodynamics and mass transfer in regular film apparatuses containing flat irrigated channels with a laminar flow of gas and liquid as the principal element are studied. The problem is solved by the approximate method, which makes it possible to drastically decrease the amount of the required calculations. It is proven that it is sufficient to determine the dimensionless flux as the function of dimensionless length in a restricted domain of parameters. Approximations are permissible outside the bounds of this domain: in some cases the changes of concentrations in phases along the crosswise direction can be neglected and, in other instances, the concentration changes can be neglected in the whole active mass-transfer region; i.e., diffusion layers exist in one or another phase before the estimation of concentration equilibrium in the system. Finally, the mass transfer resistance is concentrated in liquid or gas; there are parameter spaces where the change of concentration in one of the phases in a crosswise direction can be neglected, while another one contains diffusion boundary layers. Enthalten in Theoretical foundations of chemical engineering Moscow : MAIK Nauka/Interperiodica Publ., 2000 53(2019), 6 vom: Nov., Seite 984-995 (DE-627)332339645 (DE-600)2053532-6 1608-3431 nnns volume:53 year:2019 number:6 month:11 pages:984-995 https://dx.doi.org/10.1134/S0040579519050269 lizenzpflichtig Volltext GBV_USEFLAG_A SYSFLAG_A GBV_SPRINGER SSG-OLC-PHA GBV_ILN_11 GBV_ILN_20 GBV_ILN_22 GBV_ILN_23 GBV_ILN_24 GBV_ILN_31 GBV_ILN_32 GBV_ILN_39 GBV_ILN_40 GBV_ILN_60 GBV_ILN_62 GBV_ILN_63 GBV_ILN_69 GBV_ILN_70 GBV_ILN_73 GBV_ILN_74 GBV_ILN_90 GBV_ILN_95 GBV_ILN_100 GBV_ILN_105 GBV_ILN_110 GBV_ILN_120 GBV_ILN_138 GBV_ILN_150 GBV_ILN_151 GBV_ILN_152 GBV_ILN_161 GBV_ILN_170 GBV_ILN_171 GBV_ILN_187 GBV_ILN_206 GBV_ILN_213 GBV_ILN_224 GBV_ILN_230 GBV_ILN_250 GBV_ILN_281 GBV_ILN_285 GBV_ILN_293 GBV_ILN_370 GBV_ILN_602 GBV_ILN_636 GBV_ILN_702 GBV_ILN_2001 GBV_ILN_2003 GBV_ILN_2004 GBV_ILN_2005 GBV_ILN_2006 GBV_ILN_2007 GBV_ILN_2008 GBV_ILN_2009 GBV_ILN_2010 GBV_ILN_2011 GBV_ILN_2014 GBV_ILN_2015 GBV_ILN_2020 GBV_ILN_2021 GBV_ILN_2025 GBV_ILN_2026 GBV_ILN_2027 GBV_ILN_2031 GBV_ILN_2034 GBV_ILN_2037 GBV_ILN_2038 GBV_ILN_2039 GBV_ILN_2044 GBV_ILN_2048 GBV_ILN_2049 GBV_ILN_2050 GBV_ILN_2055 GBV_ILN_2056 GBV_ILN_2057 GBV_ILN_2059 GBV_ILN_2061 GBV_ILN_2064 GBV_ILN_2065 GBV_ILN_2068 GBV_ILN_2070 GBV_ILN_2086 GBV_ILN_2088 GBV_ILN_2093 GBV_ILN_2106 GBV_ILN_2107 GBV_ILN_2108 GBV_ILN_2110 GBV_ILN_2111 GBV_ILN_2112 GBV_ILN_2113 GBV_ILN_2116 GBV_ILN_2118 GBV_ILN_2119 GBV_ILN_2122 GBV_ILN_2129 GBV_ILN_2143 GBV_ILN_2144 GBV_ILN_2147 GBV_ILN_2148 GBV_ILN_2152 GBV_ILN_2153 GBV_ILN_2188 GBV_ILN_2190 GBV_ILN_2232 GBV_ILN_2336 GBV_ILN_2446 GBV_ILN_2470 GBV_ILN_2472 GBV_ILN_2507 GBV_ILN_2522 GBV_ILN_2548 GBV_ILN_4035 GBV_ILN_4037 GBV_ILN_4046 GBV_ILN_4112 GBV_ILN_4125 GBV_ILN_4242 GBV_ILN_4246 GBV_ILN_4249 GBV_ILN_4251 GBV_ILN_4305 GBV_ILN_4306 GBV_ILN_4307 GBV_ILN_4313 GBV_ILN_4322 GBV_ILN_4323 GBV_ILN_4324 GBV_ILN_4325 GBV_ILN_4326 GBV_ILN_4333 GBV_ILN_4334 GBV_ILN_4335 GBV_ILN_4336 GBV_ILN_4338 GBV_ILN_4393 GBV_ILN_4700 58.00 ASE AR 53 2019 6 11 984-995
allfieldsSound	10.1134/S0040579519050269 doi (DE-627)SPR017987660 (SPR)S0040579519050269-e DE-627 ger DE-627 rakwb eng 660 ASE 58.00 bkl Babak, V. N. verfasserin aut Mass Transfer in Irrigated Plane-Parallel Channels at Uniflow Laminar Motion of Liquid and Gas 2019 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier Abstract Hydrodynamics and mass transfer in regular film apparatuses containing flat irrigated channels with a laminar flow of gas and liquid as the principal element are studied. The problem is solved by the approximate method, which makes it possible to drastically decrease the amount of the required calculations. It is proven that it is sufficient to determine the dimensionless flux as the function of dimensionless length in a restricted domain of parameters. Approximations are permissible outside the bounds of this domain: in some cases the changes of concentrations in phases along the crosswise direction can be neglected and, in other instances, the concentration changes can be neglected in the whole active mass-transfer region; i.e., diffusion layers exist in one or another phase before the estimation of concentration equilibrium in the system. Finally, the mass transfer resistance is concentrated in liquid or gas; there are parameter spaces where the change of concentration in one of the phases in a crosswise direction can be neglected, while another one contains diffusion boundary layers. Enthalten in Theoretical foundations of chemical engineering Moscow : MAIK Nauka/Interperiodica Publ., 2000 53(2019), 6 vom: Nov., Seite 984-995 (DE-627)332339645 (DE-600)2053532-6 1608-3431 nnns volume:53 year:2019 number:6 month:11 pages:984-995 https://dx.doi.org/10.1134/S0040579519050269 lizenzpflichtig Volltext GBV_USEFLAG_A SYSFLAG_A GBV_SPRINGER SSG-OLC-PHA GBV_ILN_11 GBV_ILN_20 GBV_ILN_22 GBV_ILN_23 GBV_ILN_24 GBV_ILN_31 GBV_ILN_32 GBV_ILN_39 GBV_ILN_40 GBV_ILN_60 GBV_ILN_62 GBV_ILN_63 GBV_ILN_69 GBV_ILN_70 GBV_ILN_73 GBV_ILN_74 GBV_ILN_90 GBV_ILN_95 GBV_ILN_100 GBV_ILN_105 GBV_ILN_110 GBV_ILN_120 GBV_ILN_138 GBV_ILN_150 GBV_ILN_151 GBV_ILN_152 GBV_ILN_161 GBV_ILN_170 GBV_ILN_171 GBV_ILN_187 GBV_ILN_206 GBV_ILN_213 GBV_ILN_224 GBV_ILN_230 GBV_ILN_250 GBV_ILN_281 GBV_ILN_285 GBV_ILN_293 GBV_ILN_370 GBV_ILN_602 GBV_ILN_636 GBV_ILN_702 GBV_ILN_2001 GBV_ILN_2003 GBV_ILN_2004 GBV_ILN_2005 GBV_ILN_2006 GBV_ILN_2007 GBV_ILN_2008 GBV_ILN_2009 GBV_ILN_2010 GBV_ILN_2011 GBV_ILN_2014 GBV_ILN_2015 GBV_ILN_2020 GBV_ILN_2021 GBV_ILN_2025 GBV_ILN_2026 GBV_ILN_2027 GBV_ILN_2031 GBV_ILN_2034 GBV_ILN_2037 GBV_ILN_2038 GBV_ILN_2039 GBV_ILN_2044 GBV_ILN_2048 GBV_ILN_2049 GBV_ILN_2050 GBV_ILN_2055 GBV_ILN_2056 GBV_ILN_2057 GBV_ILN_2059 GBV_ILN_2061 GBV_ILN_2064 GBV_ILN_2065 GBV_ILN_2068 GBV_ILN_2070 GBV_ILN_2086 GBV_ILN_2088 GBV_ILN_2093 GBV_ILN_2106 GBV_ILN_2107 GBV_ILN_2108 GBV_ILN_2110 GBV_ILN_2111 GBV_ILN_2112 GBV_ILN_2113 GBV_ILN_2116 GBV_ILN_2118 GBV_ILN_2119 GBV_ILN_2122 GBV_ILN_2129 GBV_ILN_2143 GBV_ILN_2144 GBV_ILN_2147 GBV_ILN_2148 GBV_ILN_2152 GBV_ILN_2153 GBV_ILN_2188 GBV_ILN_2190 GBV_ILN_2232 GBV_ILN_2336 GBV_ILN_2446 GBV_ILN_2470 GBV_ILN_2472 GBV_ILN_2507 GBV_ILN_2522 GBV_ILN_2548 GBV_ILN_4035 GBV_ILN_4037 GBV_ILN_4046 GBV_ILN_4112 GBV_ILN_4125 GBV_ILN_4242 GBV_ILN_4246 GBV_ILN_4249 GBV_ILN_4251 GBV_ILN_4305 GBV_ILN_4306 GBV_ILN_4307 GBV_ILN_4313 GBV_ILN_4322 GBV_ILN_4323 GBV_ILN_4324 GBV_ILN_4325 GBV_ILN_4326 GBV_ILN_4333 GBV_ILN_4334 GBV_ILN_4335 GBV_ILN_4336 GBV_ILN_4338 GBV_ILN_4393 GBV_ILN_4700 58.00 ASE AR 53 2019 6 11 984-995
language	English
source	Enthalten in Theoretical foundations of chemical engineering 53(2019), 6 vom: Nov., Seite 984-995 volume:53 year:2019 number:6 month:11 pages:984-995
sourceStr	Enthalten in Theoretical foundations of chemical engineering 53(2019), 6 vom: Nov., Seite 984-995 volume:53 year:2019 number:6 month:11 pages:984-995
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container_title	Theoretical foundations of chemical engineering
authorswithroles_txt_mv	Babak, V. N. @@aut@@
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author	Babak, V. N.
spellingShingle	Babak, V. N. ddc 660 bkl 58.00 Mass Transfer in Irrigated Plane-Parallel Channels at Uniflow Laminar Motion of Liquid and Gas
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topic_title	660 ASE 58.00 bkl Mass Transfer in Irrigated Plane-Parallel Channels at Uniflow Laminar Motion of Liquid and Gas
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title	Mass Transfer in Irrigated Plane-Parallel Channels at Uniflow Laminar Motion of Liquid and Gas
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title_full	Mass Transfer in Irrigated Plane-Parallel Channels at Uniflow Laminar Motion of Liquid and Gas
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title_sort	mass transfer in irrigated plane-parallel channels at uniflow laminar motion of liquid and gas
title_auth	Mass Transfer in Irrigated Plane-Parallel Channels at Uniflow Laminar Motion of Liquid and Gas
abstract	Abstract Hydrodynamics and mass transfer in regular film apparatuses containing flat irrigated channels with a laminar flow of gas and liquid as the principal element are studied. The problem is solved by the approximate method, which makes it possible to drastically decrease the amount of the required calculations. It is proven that it is sufficient to determine the dimensionless flux as the function of dimensionless length in a restricted domain of parameters. Approximations are permissible outside the bounds of this domain: in some cases the changes of concentrations in phases along the crosswise direction can be neglected and, in other instances, the concentration changes can be neglected in the whole active mass-transfer region; i.e., diffusion layers exist in one or another phase before the estimation of concentration equilibrium in the system. Finally, the mass transfer resistance is concentrated in liquid or gas; there are parameter spaces where the change of concentration in one of the phases in a crosswise direction can be neglected, while another one contains diffusion boundary layers.
abstractGer	Abstract Hydrodynamics and mass transfer in regular film apparatuses containing flat irrigated channels with a laminar flow of gas and liquid as the principal element are studied. The problem is solved by the approximate method, which makes it possible to drastically decrease the amount of the required calculations. It is proven that it is sufficient to determine the dimensionless flux as the function of dimensionless length in a restricted domain of parameters. Approximations are permissible outside the bounds of this domain: in some cases the changes of concentrations in phases along the crosswise direction can be neglected and, in other instances, the concentration changes can be neglected in the whole active mass-transfer region; i.e., diffusion layers exist in one or another phase before the estimation of concentration equilibrium in the system. Finally, the mass transfer resistance is concentrated in liquid or gas; there are parameter spaces where the change of concentration in one of the phases in a crosswise direction can be neglected, while another one contains diffusion boundary layers.
abstract_unstemmed	Abstract Hydrodynamics and mass transfer in regular film apparatuses containing flat irrigated channels with a laminar flow of gas and liquid as the principal element are studied. The problem is solved by the approximate method, which makes it possible to drastically decrease the amount of the required calculations. It is proven that it is sufficient to determine the dimensionless flux as the function of dimensionless length in a restricted domain of parameters. Approximations are permissible outside the bounds of this domain: in some cases the changes of concentrations in phases along the crosswise direction can be neglected and, in other instances, the concentration changes can be neglected in the whole active mass-transfer region; i.e., diffusion layers exist in one or another phase before the estimation of concentration equilibrium in the system. Finally, the mass transfer resistance is concentrated in liquid or gas; there are parameter spaces where the change of concentration in one of the phases in a crosswise direction can be neglected, while another one contains diffusion boundary layers.
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title_short	Mass Transfer in Irrigated Plane-Parallel Channels at Uniflow Laminar Motion of Liquid and Gas
url	https://dx.doi.org/10.1134/S0040579519050269
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up_date	2024-07-03T16:32:25.035Z
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N.</subfield><subfield code="e">verfasserin</subfield><subfield code="4">aut</subfield></datafield><datafield tag="245" ind1="1" ind2="0"><subfield code="a">Mass Transfer in Irrigated Plane-Parallel Channels at Uniflow Laminar Motion of Liquid and Gas</subfield></datafield><datafield tag="264" ind1=" " ind2="1"><subfield code="c">2019</subfield></datafield><datafield tag="336" ind1=" " ind2=" "><subfield code="a">Text</subfield><subfield code="b">txt</subfield><subfield code="2">rdacontent</subfield></datafield><datafield tag="337" ind1=" " ind2=" "><subfield code="a">Computermedien</subfield><subfield code="b">c</subfield><subfield code="2">rdamedia</subfield></datafield><datafield tag="338" ind1=" " ind2=" "><subfield code="a">Online-Ressource</subfield><subfield code="b">cr</subfield><subfield code="2">rdacarrier</subfield></datafield><datafield tag="520" ind1=" " ind2=" "><subfield code="a">Abstract Hydrodynamics and mass transfer in regular film apparatuses containing flat irrigated channels with a laminar flow of gas and liquid as the principal element are studied. The problem is solved by the approximate method, which makes it possible to drastically decrease the amount of the required calculations. It is proven that it is sufficient to determine the dimensionless flux as the function of dimensionless length in a restricted domain of parameters. Approximations are permissible outside the bounds of this domain: in some cases the changes of concentrations in phases along the crosswise direction can be neglected and, in other instances, the concentration changes can be neglected in the whole active mass-transfer region; i.e., diffusion layers exist in one or another phase before the estimation of concentration equilibrium in the system. 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Mass Transfer in Irrigated Plane-Parallel Channels at Uniflow Laminar Motion of Liquid and Gas

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